EP0096149A1 - Procédé et dispositif pour éliminer des particules en suspension de gaz - Google Patents

Procédé et dispositif pour éliminer des particules en suspension de gaz Download PDF

Info

Publication number
EP0096149A1
EP0096149A1 EP83100466A EP83100466A EP0096149A1 EP 0096149 A1 EP0096149 A1 EP 0096149A1 EP 83100466 A EP83100466 A EP 83100466A EP 83100466 A EP83100466 A EP 83100466A EP 0096149 A1 EP0096149 A1 EP 0096149A1
Authority
EP
European Patent Office
Prior art keywords
gas
chamber
washing liquid
shaft
tangential
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP83100466A
Other languages
German (de)
English (en)
Other versions
EP0096149B1 (fr
Inventor
Norbert Kijowsky
Jürgen Dipl.-Ing. Seipenbusch
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hugo Petersen GmbH
Original Assignee
Hugo Petersen GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hugo Petersen GmbH filed Critical Hugo Petersen GmbH
Priority to AT83100466T priority Critical patent/ATE23453T1/de
Publication of EP0096149A1 publication Critical patent/EP0096149A1/fr
Application granted granted Critical
Publication of EP0096149B1 publication Critical patent/EP0096149B1/fr
Expired legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D47/00Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/16Apparatus having rotary means, other than rotatable nozzles, for atomising the cleaning liquid
    • B01D47/18Apparatus having rotary means, other than rotatable nozzles, for atomising the cleaning liquid with horizontally-arranged shafts

Definitions

  • the invention relates to a method for removing suspended matter from gases in a chamber with tangential gas inlet and axial gas outlet or axial gas inlet and tangential gas outlet, an axis-centric rotary atomizing device by means of which washing liquid is introduced into the gas stream in droplet form and brought into contact with the suspended matter. It also relates to devices for performing the method.
  • DE-AS 1 o35 621 describes a gas preparation stage, referred to as a humidification chamber, through which the gas to be treated flows axially, with a certain rotational movement being impressed on the gas by tangential entry and exit.
  • the washing liquid is atomized very finely by an atomizing device.
  • the atomizer device is arranged in the center of the axis and, according to the illustration, consists of several rotating atomizer disks, the top of which is acted upon by washing liquid.
  • the function of the other panes is not clear from the illustration. This procedure has the disadvantage that the advantages of the rotary movement of the gas due to the essentially axial gas routing are not used consistently.
  • the insufficient effectiveness for the separation of suspended matter is also proven by the use only as a humidification and preparation chamber.
  • the invention has for its object to treat gases loaded with suspended matter in a chamber with a washing liquid so that the contact -washing liquid / gas suspended material- is optimized by targeted system-internal measures and centrifugal means.
  • a method is proposed according to the invention, which is characterized in that the washing liquid is introduced evenly distributed over the entire chamber depth into the gas stream, the washing liquid amount is 1.5 11m3 to lo l / m 3 gas and the washing liquid entry in the gas flow takes place at a speed of 2o m / s to 12o m / s.
  • the peripheral speed used is advantageously between 20 m / s and 120 m / s, preferably between 50 m / s and 80 m / s.
  • washing liquid drops in the treatment chamber in connection with a maximum suspended matter separation
  • 1.5 l / m 3 - lo 11m3 of gas to be treated has resulted.
  • the smaller amount of washing liquid is selected in combination with a small average drop size and high peripheral speed of the atomizing plate or cup and vice versa.
  • a device which is characterized in that the individual elements of the rotary atomizer in plate or cup shape are arranged at a distance of 2 mm-10 mm from one another and in their entirety fill the chamber depth.
  • the rotary atomizer elements are arranged on a hollow shaft.
  • the hollow shaft space serves as a feed for the washing liquid.
  • a radial blower impeller is additionally arranged in the chamber, which can be driven by the rotary atomizer shaft or by a shaft independent of it.
  • the treatment chamber in which the method according to the invention runs and in which the aids for carrying out the method are integrated consists of two flat boundary walls perpendicular to the axis of rotation of the gas flow, a spirally expanded or cylindrical boundary wall that is perpendicular to the flat boundary walls stands, the tangential outlet or inlet opening for the gas extending over the entire depth of the chamber.
  • the gas to be treated is fed axially through a treatment chamber 1 through the inlet nozzle 2, which widens conically towards the chamber 1.
  • the washing liquid passes via the pipe 3 practically without pressure from the front part of the shaft 5, which is designed as a hollow shaft and is driven directly or indirectly by a motor 4, on which atomizing plates 6 are fastened at a short distance from one another.
  • the washing liquid reaches the atomizing plate 6 in a uniform distribution, is accelerated there to the circumference as a result of the rotary movement of the atomizing plate 6, and from there, divided into drops, is thrown into the chamber 1.
  • the direction of rotation of the atomizing disks can be chosen to be opposite or, preferably, the same as the direction of rotation of the gas flow, the rotating gas movement resulting from the tangential arrangement of the gas outlet connection 8.
  • the gas to be treated enters the treatment chamber 1 axially through the nozzle 2 and is set in a rapid rotary movement there by the rotating blades 10 attached to the impeller 9.
  • the transfer of the rotary movement to the gas is supported by the washing liquid drops thrown off by the cups 6 of the atomizing device driven by the shaft 5.
  • the bladed impeller 9 is also driven by the motor 4 via the shaft 5.
  • the washing liquid is fed to the atomizer cups 6 via the pipeline 3, from which it reaches the shaft 5, which is designed as a hollow shaft in the front part, and reaches the atomizer cups 6 through the recesses 7.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Nozzles (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
EP83100466A 1982-05-21 1983-01-20 Procédé et dispositif pour éliminer des particules en suspension de gaz Expired EP0096149B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT83100466T ATE23453T1 (de) 1982-05-21 1983-01-20 Verfahren und vorrichtung zum entfernen von schwebestoffen aus gasen.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3219088 1982-05-21
DE3219088A DE3219088C1 (de) 1982-05-21 1982-05-21 Verfahren und Vorrichtung zum Entfernen von Schwebestoffen aus Gasen

Publications (2)

Publication Number Publication Date
EP0096149A1 true EP0096149A1 (fr) 1983-12-21
EP0096149B1 EP0096149B1 (fr) 1986-11-12

Family

ID=6164146

Family Applications (1)

Application Number Title Priority Date Filing Date
EP83100466A Expired EP0096149B1 (fr) 1982-05-21 1983-01-20 Procédé et dispositif pour éliminer des particules en suspension de gaz

Country Status (4)

Country Link
EP (1) EP0096149B1 (fr)
AT (1) ATE23453T1 (fr)
DE (1) DE3219088C1 (fr)
ES (1) ES8402168A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993000150A1 (fr) * 1991-06-28 1993-01-07 Harald Hackl Dispositif de lavage de gaz de fumee

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2518769C1 (ru) * 2013-01-23 2014-06-10 Александр Олегович Кудрявцев Турбонасос для двух текучих сред

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2235998A (en) * 1939-07-15 1941-03-25 Pease Anthony Equipment Compan Apparatus for producing an intimate contact between a liquid and a gas
DE1035621B (de) * 1951-10-31 1958-08-07 Antoine Planaguma Einrichtung zum Entfernen von feinen Fluessigkeitsteilchen aus Gasen
DE2015737B2 (de) * 1969-07-05 1980-09-25 Hugo Petersen Gesellschaft Fuer Verfahrenstechnischen Anlagenbau Mbh & Co Kg, 6200 Wiesbaden Vorrichtung zur Agglomeration und Niederschlagung von Schwebestoffen aus Gasen und Dämpfen und/oder zur Absorption von Gasbestandteilen

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2235998A (en) * 1939-07-15 1941-03-25 Pease Anthony Equipment Compan Apparatus for producing an intimate contact between a liquid and a gas
DE1035621B (de) * 1951-10-31 1958-08-07 Antoine Planaguma Einrichtung zum Entfernen von feinen Fluessigkeitsteilchen aus Gasen
DE2015737B2 (de) * 1969-07-05 1980-09-25 Hugo Petersen Gesellschaft Fuer Verfahrenstechnischen Anlagenbau Mbh & Co Kg, 6200 Wiesbaden Vorrichtung zur Agglomeration und Niederschlagung von Schwebestoffen aus Gasen und Dämpfen und/oder zur Absorption von Gasbestandteilen

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993000150A1 (fr) * 1991-06-28 1993-01-07 Harald Hackl Dispositif de lavage de gaz de fumee
US5480463A (en) * 1991-06-28 1996-01-02 Hackl; Harald Apparatus for flue gas cleaning

Also Published As

Publication number Publication date
EP0096149B1 (fr) 1986-11-12
ES522054A0 (es) 1984-02-01
ES8402168A1 (es) 1984-02-01
ATE23453T1 (de) 1986-11-15
DE3219088C1 (de) 1983-11-17

Similar Documents

Publication Publication Date Title
US4116163A (en) Apparatus to coat a flowing mass of particulate material
DE3152066A1 (en) Centrifugal separator
EP0190688A2 (fr) Procédé et dispositif de purification de gaz de fumée avec un absorbant fluide d'après le principe de la pulvérisation du courant d'air
DE2814958A1 (de) Mikromahlmischer
DE102007000708A1 (de) Entlüfter mit eine vertikal verteilte Medienabschleuderung vorsehendem Schleuderteller
EP0035705A2 (fr) Séparateur d'écume et procédé d'utilisation
CH646614A5 (de) Wirbelschichtapparatur.
DE3219088C1 (de) Verfahren und Vorrichtung zum Entfernen von Schwebestoffen aus Gasen
EP4041433A1 (fr) Dispositif d'épuration de gaz
DE10217967C1 (de) Filtervorrichtung zur Filterung von Fluiden
EP0331809A1 (fr) Dispositif et procédé pour séparer des aérosols dans des gaz d'échappement
DE2335339C3 (de) Vorrichtung zum Beseitigen bzw. Abscheiden von Staub- und Dunstteilchen aus einem Gas
CH355770A (de) Verfahren und Apparatur zur kontinuierlichen oder chargenweisen Behandlung von Stoffen und Stoffgemischen
DE2235561C3 (de) Verfahren und Vorrichtung zur Reinigung eines Gases
DE2739286C3 (de) Strahlmittel aus Siliziumdioxidsand oder Schlacke und Verfahren zu dessen Herstellung
DE622123C (de) Einrichtung zum stufenweisen Zerstaeuben von Fluessigkeiten mittels eines umlaufenden Fliehkraftzerstaeubers in dampf- oder gasfoermigen Stoffen
DE2356042C3 (de) Vorrichtung zum Einmaischen feinfaseriger Feststoffe mit einer Lösung
DE2024098C3 (de) Verfahren und Vorrichtung zum Agglomerieren und Niederschlagen von Schwebestoffen aus Gasen und Dämpfen
DE725871C (de) Milcherhitzer mit Trommelruehrwerk
DE1471602A1 (de) Gaswaschanlage
DE473455C (de) Verfahren und Vorrichtung zum Zerstaeuben und Ausbreiten fluessiger, breiiger, geschmolzener und aehnlicher Stoffe
DE1262921B (de) Verfahren und Vorrichtung zur Behandlung von Feststoff- oder Fluessigkeitsteilchen in einem Fliehkraftfeld
DE1125623B (de) Vorrichtung zum Befeuchten von Luft
CH433197A (de) Gasreinigungseinrichtung
AT263526B (de) Vorrichtung zur Behandlung von aus Pflanzenprodukten stammenden Pasten mittels Bleichungsreagentien

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 19830214

AK Designated contracting states

Designated state(s): AT BE CH FR GB IT LI NL SE

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH FR GB IT LI NL SE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 19861112

Ref country code: FR

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 19861112

REF Corresponds to:

Ref document number: 23453

Country of ref document: AT

Date of ref document: 19861115

Kind code of ref document: T

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SE

Effective date: 19861130

EN Fr: translation not filed
PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

GBPC Gb: european patent ceased through non-payment of renewal fee
26N No opposition filed
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19881122

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: CH

Payment date: 19920123

Year of fee payment: 10

Ref country code: AT

Payment date: 19920123

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19920131

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 19920303

Year of fee payment: 10

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Effective date: 19930120

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Effective date: 19930131

Ref country code: CH

Effective date: 19930131

Ref country code: BE

Effective date: 19930131

BERE Be: lapsed

Owner name: HUGO PETERSEN G. FUR VERFAHRENSTECHN. ANLAGENBAU

Effective date: 19930131

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19930801

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee
REG Reference to a national code

Ref country code: CH

Ref legal event code: PL